CN1927921B - Lithium ion conducting gel film containing porous polymer framework and preparation method thereof - Google Patents
Lithium ion conducting gel film containing porous polymer framework and preparation method thereof Download PDFInfo
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- 229910001416 lithium ion Inorganic materials 0.000 title claims abstract description 84
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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Abstract
本发明公开了一种含有多孔聚合物骨架的锂离子导电凝胶膜及其制备方法。它具有改性聚合物多孔膜骨架,在改性聚合物多孔膜骨架内填充由锂盐、稀释剂、交联聚醚进行交联反应制得。制备方法步骤:(1)采用相转化法制备聚丙二醇改性的聚偏氟乙烯或聚醚砜多孔膜;(2)在10-20℃下将碳酸酯、锂盐、聚乙二醇和二异氰酸酯混合制备成电解液;(3)在10-20℃下将多孔膜在电解液中浸泡10-30分钟吸收电解液;(4)将吸附盐电解液的多孔膜在60℃下处理8-10小时进行交联凝胶化。该法操作和应用方便,得到的凝胶膜具有强度高、形状稳定、锂盐电解质负载率高,导电率在10-3~10-2S/cm之间,适合于隔膜与电解质一体化的聚合物锂离子电池使用。The invention discloses a lithium ion conductive gel film containing a porous polymer skeleton and a preparation method thereof. It has a modified polymer porous membrane skeleton, which is filled with lithium salt, diluent, and crosslinked polyether to carry out crosslinking reaction in the modified polymer porous membrane skeleton. The steps of the preparation method: (1) preparing polypropylene glycol-modified polyvinylidene fluoride or polyethersulfone porous membrane by phase inversion method; (2) mixing carbonate, lithium salt, polyethylene glycol and diisocyanate at 10-20°C Mix to prepare an electrolyte; (3) Soak the porous membrane in the electrolyte for 10-30 minutes at 10-20°C to absorb the electrolyte; (4) Treat the porous membrane that absorbs the salt electrolyte at 60°C for 8-10 minutes Hours for cross-linking and gelation. This method is easy to operate and apply, and the obtained gel film has high strength, stable shape, high loading rate of lithium salt electrolyte, and conductivity between 10 -3 and 10 -2 S/cm, which is suitable for the integration of diaphragm and electrolyte Polymer lithium ion battery is used.
Description
技术领域technical field
本发明属于聚合物电解质技术领域,特别涉及一种含有多孔聚合物骨架的锂离子导电凝胶膜及其制备方法。The invention belongs to the technical field of polymer electrolytes, in particular to a lithium ion conductive gel film containing a porous polymer skeleton and a preparation method thereof.
背景技术Background technique
锂离子电池又称锂二次电池,是一种可充电二次电源,具有比能量高、电性能优良、可以制成多种形状等特点,广泛地应用于移动电话、电动汽车、笔记本电脑、照相/摄相等需要便携式电源的领域。随着相关产业的需求的持续增长,锂离子电池材料和技术正处于迅速发展的阶段。提高锂离子电池的安全性、能量密度和使用长寿命是的高性能锂电池的发展方向。在锂离子电池的核心材料与技术中,电极间电解质体系的种类和性能对电池结构与制作技术、电池的内阻、充放电电流密度、充放电循环特性、离子电导率、电化学窗口、不漏液与抗过充放电安全性等方面具有决定性影响,是锂离子电池的关键和核心之一,过去的20年中,锂离子电池技术和进展几乎是其中电解质体系所决定的。根据电解质体系的不同,锂离子电池技术的发展历程大致可分为液体锂离子电池、固态锂离子电池、凝胶锂离子电池三个发展阶段。Lithium-ion battery, also known as lithium secondary battery, is a rechargeable secondary power supply with high specific energy, excellent electrical performance, and can be made into various shapes. It is widely used in mobile phones, electric vehicles, notebook computers, Fields that require portable power such as photography/photography. With the continuous growth of demand in related industries, lithium-ion battery materials and technologies are in a stage of rapid development. Improving the safety, energy density and long life of lithium-ion batteries is the development direction of high-performance lithium batteries. In the core materials and technologies of lithium-ion batteries, the type and performance of the electrolyte system between electrodes has a great influence on the battery structure and manufacturing technology, internal resistance of the battery, charge-discharge current density, charge-discharge cycle characteristics, ionic conductivity, electrochemical window, different Leakage and anti-overcharge and discharge safety have a decisive impact, and it is one of the keys and cores of lithium-ion batteries. In the past 20 years, the technology and progress of lithium-ion batteries are almost determined by the electrolyte system. According to different electrolyte systems, the development of lithium-ion battery technology can be roughly divided into three stages of development: liquid lithium-ion batteries, solid-state lithium-ion batteries, and gel lithium-ion batteries.
液体锂离子电池技术采用电解质体系是以热致相分离法制备的聚乙烯单层微孔膜、或熔融成型-拉伸成孔法制备聚丙烯单层微孔膜或聚丙烯/聚乙烯多层复合微孔膜为电极间隔膜,膜的孔径在0.5μm、厚度在20-30μm,膜内填充液体的锂盐电解液,相关的专利如US 3801404,US 3558764,US 3843761,US 5691047等。这类以液体为电解质的技术是目前锂电池产品中应用最广泛的技术,但是存在聚乙烯和聚丙烯质材的隔膜与孔隙率较低、电解液的亲合性能不好、液体电解质容易渗漏等问题,进而产生内阻大、能量密度低、性能衰减快、安全性低等不利结果。The liquid lithium-ion battery technology adopts the electrolyte system to prepare a polyethylene single-layer microporous membrane by a thermally induced phase separation method, or a polypropylene single-layer microporous membrane or a polypropylene/polyethylene multilayer by a melt-forming-stretching pore-forming method. The composite microporous membrane is an electrode separator membrane with a pore size of 0.5 μm and a thickness of 20-30 μm. The membrane is filled with a liquid lithium salt electrolyte. Related patents such as US 3801404, US 3558764, US 3843761, US 5691047, etc. This kind of technology using liquid as electrolyte is currently the most widely used technology in lithium battery products, but there are separators made of polyethylene and polypropylene with low porosity, poor affinity for electrolyte, and easy penetration of liquid electrolyte. Leakage and other problems, resulting in adverse results such as large internal resistance, low energy density, fast performance decay, and low safety.
固态锂离子电池技术是采用具有锂离子导电作用的聚合物复合膜作为电极间电解质,其基本原理是采用聚环氧乙烷中的氧络合锂离子、锂离子在柔性聚环氧乙烷中跃迁锂离子导电。典型的制备方法是将聚环氧乙烷和锂盐、溶剂混合成溶液,溶液成膜使溶剂蒸发得到含有锂离子聚环氧乙烷复合膜(如:Feuilade G,J Appl Electrochem,1795,63;Appetecchi G B,JElectrochem Soc,2001,A1171;Appetecchi G B,J Electrochem Soc,2002,A891等)。由于聚环氧乙烷膜的强度低,也提出了通过采用聚甲基丙烯酸甲酯、聚苯乙烯、聚丙烯腈等聚合物与聚环氧乙烷共混、接枝或交联技术制备固体锂离子复合膜的方法(如:W Wieczorek,Electrochim,1992,1565;Z Florjanczyk,Polymer,1991,3422;Z Florjanczyk,Pure Appl.Chem, 1992,853;Y Kato,Solid State Ionics,2001,155;付延鲍,电源技术,2002,47等)。与液体锂离子电池中电解质体系相比,固态锂离子电池技术的主要特点是聚合物电解质具有电解质和隔膜双重作用,从体积小、质量轻、寿命长、安全性能高、易于电池形状设计的要求看有明显的优势,但是由于聚合物复合膜的导率太低(远远小于10-3S/cm),目前还达不到实际应用的要求。Solid-state lithium-ion battery technology uses a polymer composite film with lithium ion conductivity as the electrolyte between electrodes. The basic principle is to use oxygen complexed lithium ions in polyethylene oxide, and lithium ions in flexible polyethylene oxide Transition lithium ions conduct electricity. A typical preparation method is that polyethylene oxide, lithium salt, and solvent are mixed into a solution, and the solution is formed into a film to evaporate the solvent to obtain a polyethylene oxide composite film containing lithium ions (such as: Feuilade G, J Appl Electrochem, 1795, 63 ; Appetecchi G B, J Electrochem Soc, 2001, A1171; Appetecchi G B, J Electrochem Soc, 2002, A891, etc.). Due to the low strength of polyethylene oxide film, it is also proposed to prepare solid film by blending, grafting or crosslinking polymers such as polymethyl methacrylate, polystyrene, polyacrylonitrile and polyethylene oxide. The method of lithium ion composite membrane (such as: W Wieczorek, Electrochim, 1992,1565; Z Florjanczyk, Polymer, 1991,3422; Z Florjanczyk, Pure Appl.Chem, 1992,853; Y Kato, Solid State Ionics, 2001,155; Fu Yanbao, Power Technology, 2002, 47, etc.). Compared with the electrolyte system in liquid lithium-ion batteries, the main feature of solid-state lithium-ion battery technology is that the polymer electrolyte has the dual functions of electrolyte and diaphragm, from the requirements of small size, light weight, long life, high safety performance, and easy battery shape design It seems that there are obvious advantages, but because the conductivity of the polymer composite membrane is too low (far less than 10 -3 S/cm), it cannot meet the requirements of practical application at present.
凝胶锂离子电池采用的含有锂离子的凝胶聚合物电解质膜作为电极间电解质材料,实质上也是一种全固态锂离子电池,与全固态锂离子电池用电解质膜相比,主要是采用在膜中添加增塑剂或稀释剂使电解质膜处于凝胶态,通过降低聚合物链结晶性、提高锂离子的迁移率和电导率。制备锂离子凝胶聚合物电解质膜的已有方法分三种。(1)共混浇铸法:将聚合物、低沸点溶剂、高沸点稀释剂/增塑剂和电解液混合成均匀的溶液,在玻璃板、不锈钢或聚酯带上流延、刮制成液膜,然后使溶剂完全挥发完得到凝胶聚合物电解质膜。操作中所有原料事先都必须经过严格干燥处理,整个过程都需在无氧无水条件下进行、工艺条件苛刻。(2)混合-聚合法:将单体、引发剂、电解液、交联剂混合成溶液注入电池,密封后引发聚合。相对于浇铸法,工艺条件苛刻程度降低,是可以直接在电极间制作凝胶聚合物电解质膜、更适合于在锂离子电池制备,但是未反应的单体和引发剂不易除去,会影响电导率和凝胶聚合物电解质的稳定性。(3)制膜一浸渍电解液法:基本过程是将聚合物(主要为聚(偏氟乙烯-六氟丙烯)、增塑剂(有时也称成孔剂)、溶剂混合后经浇铸成液膜、溶剂蒸发后得到固体膜,然后用萃取剂萃取掉增塑剂或成孔剂得到具有多孔结构聚合物骨架,最后将干燥的膜浸入锂盐电解液吸附电解质活化。由于该方法的实质是电解液的溶剂对多孔骨架有溶胀作用,导致的骨架内凝胶作用并增加电解液吸附量,但是位于孔隙中的凝胶与聚合物骨架之间的作用力很小,基本上为自由溶液,当电池内部压力升高,电解液仍会从聚合物基体中脱离出来。The gel polymer electrolyte membrane containing lithium ions used in the gel lithium-ion battery is used as the electrolyte material between the electrodes, which is essentially an all-solid-state lithium-ion battery. Compared with the electrolyte membrane for all-solid-state lithium-ion batteries, it is mainly used in Adding a plasticizer or diluent to the membrane makes the electrolyte membrane in a gel state, which reduces the crystallinity of the polymer chain and improves the mobility and conductivity of lithium ions. There are three existing methods for preparing lithium ion gel polymer electrolyte membranes. (1) Blending casting method: Mix polymer, low boiling point solvent, high boiling point diluent/plasticizer and electrolyte into a uniform solution, cast and scrape it on a glass plate, stainless steel or polyester tape to form a liquid film , and then the solvent is completely evaporated to obtain a gel polymer electrolyte membrane. All raw materials in the operation must be strictly dried in advance, and the whole process must be carried out under anaerobic and water-free conditions, and the process conditions are harsh. (2) Mixing-polymerization method: the monomer, initiator, electrolyte, and cross-linking agent are mixed into a solution and injected into the battery, and the polymerization is initiated after sealing. Compared with the casting method, the harshness of the process conditions is reduced, and the gel polymer electrolyte membrane can be directly produced between the electrodes, which is more suitable for the preparation of lithium-ion batteries, but unreacted monomers and initiators are not easy to remove, which will affect the conductivity. and the stability of the gel polymer electrolyte. (3) Membrane-impregnation electrolyte method: the basic process is to mix polymers (mainly poly(vinylidene fluoride-hexafluoropropylene), plasticizers (sometimes also called pore-forming agents), and solvents and then cast them into liquid After the membrane and the solvent are evaporated, a solid membrane is obtained, and then the plasticizer or pore-forming agent is extracted with an extractant to obtain a polymer skeleton with a porous structure, and finally the dried membrane is immersed in a lithium salt electrolyte to adsorb the electrolyte for activation. Since the essence of the method is The solvent of the electrolyte has a swelling effect on the porous skeleton, resulting in gelation in the skeleton and increasing the amount of electrolyte adsorption, but the force between the gel in the pores and the polymer skeleton is very small, and it is basically a free solution. When the internal pressure of the battery increases, the electrolyte will still be released from the polymer matrix.
采用上述三种方法制备的锂离子凝胶电解质膜的聚合物体系有聚环氧乙烷体系(如:唐致远,高分子材料科学与工程,2003,48;M Borghini,Electrochim Acta,1996,2369;Kang,JPower sources,2003,432等)、PAN体系(如:Y Matsuda,J Power Sources,2003,473;DPeramunage,Solid State Ionics,1994,79等)、PMMA体系(如H J Ryoo,Solid State Electrochem,1998,1;A M Stephan,J Power Sources,1999,752;D W Kim,J Power Sources,2000,78等)和含氟体聚合物系(如:US Patent 5418091,1995;US 5658685,1997;US 5716421,1998;US5296318和D Saikia,Phys.Stat.Sol.,2005,(a)202(2):309等)等四类。虽然这些体系凝胶聚合物电解质膜的电导率可以达到10-3S/cm以上,但实在用做锂电池电解质膜还存在以下几个方面的问题:凝胶聚合物电解质膜的强度和尺寸稳定性普遍较低,如聚甲基丙烯酸甲酯体系的体积随时间持续而明显收缩、不仅电解液流失,而且有可能脱离电极;聚苯乙烯和聚丙烯腈等聚合物与电极材料的相容性较差,体系发生分相而使电解质性能下降,并且电化学窗口下 降(如:Kim,J Power Sources,2001,102:41;Wu,Polymer,2005,5929等),即使采用共混、共聚、无机填料以及交联等手段,这些问题也难以解决。The polymer system of the lithium ion gel electrolyte membrane prepared by the above three methods has a polyethylene oxide system (such as: Tang Zhiyuan, Polymer Material Science and Engineering, 2003, 48; M Borghini, Electrochim Acta, 1996, 2369 ; Kang, JPower sources, 2003, 432 etc.), PAN system (such as: Y Matsuda, J Power Sources, 2003, 473; DPeramunage, Solid State Ionics, 1994, 79 etc.), PMMA system (such as H J Ryoo, Solid State Electrochem , 1998, 1; A M Stephan, J Power Sources, 1999, 752; D W Kim, J Power Sources, 2000, 78, etc.) and fluorine-containing polymer systems (such as: US Patent 5418091, 1995; US 5658685, 1997; US 5716421, 1998; US5296318 and D Saikia, Phys.Stat.Sol., 2005, (a) 202(2): 309, etc.) and other four categories. Although the conductivity of the gel polymer electrolyte membrane of these systems can reach more than 10 -3 S/cm, there are still some problems in the following aspects when used as the electrolyte membrane of lithium batteries: the strength and dimensional stability of the gel polymer electrolyte membrane Generally low, such as the volume of polymethyl methacrylate system continues to shrink significantly over time, not only electrolyte loss, but also may be detached from the electrode; the compatibility of polymers such as polystyrene and polyacrylonitrile with electrode materials Poor, phase separation occurs in the system and the performance of the electrolyte decreases, and the electrochemical window decreases (such as: Kim, J Power Sources, 2001, 102: 41; Wu, Polymer, 2005, 5929, etc.), even if blending, copolymerization, These problems are also difficult to solve by means of inorganic fillers and cross-linking.
偏(氟乙烯-六氟丙烯)共聚物具有良好的成膜性和机械强度、又具有高的介电常数和极好的电化学稳定性,比较适合于凝胶聚合物电解质膜使用,目前高性能凝胶聚合物电解质的研究主要以偏(氟乙烯-六氟丙烯)为基体。其中六氟丙烯链段聚集区为高弹态,具有良好的溶胀性,可吸附较多的电解液、使电导率能达到10-3S/cm,同时偏氟乙烯链段聚集区为结晶态,又赋予凝胶聚合物电解质膜良好的力学性能(吴宇平,锂离子电池:应用与实践,化学工业出版社,2004年)。单纯从GPE的综合性能看,聚偏(氟乙烯-六氟丙烯)是一种理想锂电池用凝胶聚合物电解质膜材料,但是,聚偏(氟乙烯-六氟丙烯)昂贵的价格是限制其规模化应用的主要问题。The (vinylidene fluoride-hexafluoropropylene) copolymer has good film-forming properties and mechanical strength, and has a high dielectric constant and excellent electrochemical stability. It is more suitable for the use of gel polymer electrolyte membranes. At present, high The research on performance gel polymer electrolyte is mainly based on (vinylidene fluoride-hexafluoropropylene) matrix. Among them, the hexafluoropropylene segment aggregation area is highly elastic, has good swelling property, can absorb more electrolyte, and makes the electrical conductivity reach 10 -3 S/cm, and at the same time, the vinylidene fluoride segment aggregation area is in a crystalline state , and endow the gel polymer electrolyte membrane with good mechanical properties (Wu Yuping, Lithium-ion Batteries: Application and Practice, Chemical Industry Press, 2004). Purely from the comprehensive performance of GPE, poly(vinylidene fluoride-hexafluoropropylene) is an ideal gel polymer electrolyte membrane material for lithium batteries, but the expensive price of poly(vinylidene fluoride-hexafluoropropylene) is a limitation The main problem of its large-scale application.
原理上,凝胶聚合物电解质膜的导电机理是锂离子与聚合物链上的供电子的极性基团(如氮、氧、氟等原子)配位,在电场作用下,随着聚合物高弹区中分子链段的热运动,锂离子与极性基团不断发生配位与解配位的过程,从而实现离子的迁移,即导电行为主要发生在无定型区域,而结晶区对电导率的贡献不大,为提高电导率需要降低聚合物的结晶性:另一方面,高弹态的聚合物电解质膜强度又较低,需要具有一定的结晶、交联或添加增强剂提高电解质膜的强度。因此,锂电池用凝胶聚合物电解质膜设计的原则实质可以归纳为以下几点:一是同时实现电解液吸收量高且稳定、不流失;二是聚合物基体具有足够的力学强度,热/化学稳定性好,不对电池其他部件造成损害;三是容易规模化制备和应用;四是原料成本低。In principle, the conductive mechanism of the gel polymer electrolyte membrane is that the lithium ion coordinates with the electron-donating polar groups (such as nitrogen, oxygen, fluorine, etc. atoms) on the polymer chain. The thermal movement of the molecular chain segment in the high elastic region, lithium ions and polar groups continue to undergo a process of coordination and decoordination, so as to realize the migration of ions, that is, the conduction behavior mainly occurs in the amorphous region, while the crystalline region has a great influence on the conductivity. In order to improve the conductivity, it is necessary to reduce the crystallinity of the polymer; on the other hand, the strength of the highly elastic polymer electrolyte membrane is low, and it is necessary to have a certain degree of crystallization, cross-linking or adding a reinforcing agent to improve the electrolyte membrane. Strength of. Therefore, the essence of the design principles of gel polymer electrolyte membranes for lithium batteries can be summarized as follows: first, to achieve high and stable electrolyte absorption without loss; second, the polymer matrix has sufficient mechanical strength, heat/ It has good chemical stability and does not cause damage to other battery components; third, it is easy to be prepared and applied on a large scale; and fourth, it has low cost of raw materials.
综合以上分析,在充分实验的基础上提出了一种不同于以往成分和结构的锂离子导电凝胶电解质膜,并详细地提供了这种凝胶电解质膜的制备和在锂离子电池中使用的方法。Based on the above analysis, on the basis of sufficient experiments, a lithium-ion conductive gel electrolyte membrane different from the previous composition and structure is proposed, and the preparation of this gel electrolyte membrane and its use in lithium-ion batteries are provided in detail. method.
发明内容Contents of the invention
本发明的目的是提供一种含有多孔聚合物骨架的锂离子导电凝胶膜及其制备方法。以解决现有锂离子导电凝胶电解质膜中存在电解液吸收率和保持率低、电导率低、成本高、强度差等问题,促进安全、高性能、低成本锂离子电池技术的发展。The object of the present invention is to provide a lithium ion conductive gel film containing a porous polymer skeleton and a preparation method thereof. To solve the problems of low electrolyte absorption and retention rate, low conductivity, high cost, and poor strength in the existing lithium-ion conductive gel electrolyte membrane, and promote the development of safe, high-performance, and low-cost lithium-ion battery technology.
含有多孔聚合物骨架的锂离子导电凝胶膜具有改性聚合物多孔膜骨架,在改性聚合物多孔膜骨架内填充由锂盐、稀释剂、交联聚醚进行交联反应制得的产物。The lithium-ion conductive gel membrane containing a porous polymer skeleton has a modified polymer porous membrane skeleton, and the modified polymer porous membrane skeleton is filled with a product obtained by cross-linking a lithium salt, a diluent, and a cross-linked polyether. .
所述改性聚合物多孔膜骨架由主体聚合物和改性剂组成,其中以改性聚合物多孔膜骨架总质量计主体聚合物质量百分比为70-90%,改性剂质量百分比为10-30%,主体聚合物为聚偏氟乙烯或聚醚砜,改性剂为相对数均分子质量为3000-4000的双羟基聚丙二醇。The modified polymer porous membrane skeleton is composed of a main body polymer and a modifier, wherein the weight percentage of the main body polymer is 70-90% based on the total mass of the modified polymer porous membrane skeleton, and the weight percentage of the modifier is 10-90%. 30%, the main polymer is polyvinylidene fluoride or polyethersulfone, and the modifier is dihydroxypolypropylene glycol with a relative number average molecular mass of 3000-4000.
改性聚合物多孔膜骨架的结构为:具有连续孔通道,孔径在0.2-3.0μm,孔隙率在60-80%,厚度在15-25μm。The structure of the modified polymer porous membrane skeleton is: it has continuous pore channels, the pore diameter is 0.2-3.0 μm, the porosity is 60-80%, and the thickness is 15-25 μm.
以锂盐、稀释剂与交联聚醚总质量计锂盐质量百分比为3-5%,稀释剂为20-30%,交联聚醚为65-75%。Based on the total mass of the lithium salt, the diluent and the cross-linked polyether, the mass percentage of the lithium salt is 3-5%, the diluent is 20-30%, and the cross-linked polyether is 65-75%.
交联聚醚由双羟基聚乙二醇与二异氰酸酯反应的产物,其中分子量200-1400的双羟基聚乙 二醇质量百分比为85-90%;二异氰酸酯的质量为5-10%。The cross-linked polyether is a reaction product of dihydroxypolyethylene glycol and diisocyanate, wherein the mass percentage of dihydroxypolyethylene glycol with a molecular weight of 200-1400 is 85-90%; the mass percentage of diisocyanate is 5-10%.
锂盐为六氟磷酸锂或高氯酸锂,稀释剂为碳酸二乙酯、碳酸二甲酯或碳酸甲乙烯酯,二异氰酸酯为甲苯-2,4-二异氰酸酯、二苯甲烷二异氰酸酯或异佛尔酮二异氰酸酯。The lithium salt is lithium hexafluorophosphate or lithium perchlorate, the diluent is diethyl carbonate, dimethyl carbonate or methylethylene carbonate, and the diisocyanate is toluene-2,4-diisocyanate, diphenylmethane diisocyanate or isophorone diisocyanate.
含有多孔聚合物骨架的锂离子导电凝胶膜的制备方法,包括如下步骤:The preparation method of the lithium ion conductive gel film containing porous polymer skeleton comprises the steps:
1)相转化法制备双羟基聚丙二醇改性的聚偏氟乙烯或聚醚砜多孔膜骨架;1) Preparation of dihydroxypolypropylene glycol-modified polyvinylidene fluoride or polyethersulfone porous membrane skeleton by phase inversion method;
2)将锂盐、稀释剂、双羟基聚乙二醇、二异氰酸酯在10-20℃下混合配制成电解液,其中锂盐质量百分比为3-5%,稀释剂质量百分比为20-30%,双羟基聚乙二醇质量百分比为55-70%,分子量200-1400,二异氰酸酯质量百分比为3-7%,各组分的质量百分比之和等于100%;2) Mix lithium salt, diluent, dihydroxypolyethylene glycol, and diisocyanate at 10-20°C to prepare an electrolyte solution, wherein the mass percentage of lithium salt is 3-5%, and the mass percentage of diluent is 20-30% , the mass percentage of dihydroxypolyethylene glycol is 55-70%, the molecular weight is 200-1400, the mass percentage of diisocyanate is 3-7%, and the sum of the mass percentages of each component is equal to 100%;
3)将多孔膜骨架在10-20℃的上述电解液中浸泡10-30分钟吸收电解液;3) Soak the porous membrane skeleton in the above-mentioned electrolyte at 10-20°C for 10-30 minutes to absorb the electrolyte;
4)将吸附有电解液的多孔膜骨架在60-80℃下处理8-10小时进行交联凝胶化即可。4) The porous membrane skeleton with the electrolyte absorbed is treated at 60-80° C. for 8-10 hours to carry out cross-linking and gelation.
所述的锂盐为六氟磷酸锂或高氯酸锂,稀释剂为碳酸二乙酯、碳酸二甲酯或碳酸甲乙烯酯。The lithium salt is lithium hexafluorophosphate or lithium perchlorate, and the diluent is diethyl carbonate, dimethyl carbonate or methyl vinyl carbonate.
相转化法制备双羟基聚丙二醇改性的聚偏氟乙烯或聚醚砜多孔膜骨架的步骤为:The steps of preparing polyvinylidene fluoride or polyethersulfone porous membrane skeleton modified by dihydroxypolypropylene glycol by phase inversion method are:
1)将双羟基聚丙二醇、聚乙烯吡咯烷酮、水、溶剂与聚偏氟乙烯或聚醚砜混合,在70℃下搅拌24小时,然后于30℃下真空中静置10小时脱气得到铸膜液;1) Mix dihydroxypolypropylene glycol, polyvinylpyrrolidone, water, solvent with polyvinylidene fluoride or polyethersulfone, stir at 70°C for 24 hours, and then stand in vacuum at 30°C for 10 hours to degas to obtain a cast film liquid;
2)在温度为10-30℃、相对湿度为40-80%的空气环境中,将50-60℃的铸膜液在40-50℃不锈钢板上刮制成厚度为50-150μm的液膜;2) In an air environment with a temperature of 10-30°C and a relative humidity of 40-80%, scrape the casting solution at 50-60°C on a stainless steel plate at 40-50°C to form a liquid film with a thickness of 50-150 μm ;
3)将带有液膜的不锈钢板浸入温度为30-60℃的凝固浴中并停留2-10分钟固化成膜;3) Immerse the stainless steel plate with the liquid film in a coagulation bath with a temperature of 30-60°C and stay for 2-10 minutes to solidify and form a film;
所述凝固浴组成及质量百分含量为:第一组分:水:20-100%,第二组分:对应铸膜液中用N,N’-二甲基甲酰胺或N,N’-二甲基乙酰胺溶剂:0-80%;The composition and mass percentage of the coagulation bath are as follows: the first component: water: 20-100%, the second component: corresponding to N, N'-dimethylformamide or N, N' used in the casting solution -Dimethylacetamide solvent: 0-80%;
4)将固化膜从凝固浴中取出,依次经在20-40℃的水中浸泡清洗48小时、60-80℃下干燥24小时。4) Take the cured film out of the coagulation bath, soak and wash in water at 20-40°C for 48 hours, and dry at 60-80°C for 24 hours.
铸膜液各组分及其质量百分含量为,双羟基聚聚丙二醇,1-3%,分子量为3000-4000;聚乙烯吡咯烷酮,1-4%,分子量为2×103~2×106;水:2-5%;溶剂为N,N’-二甲基甲酰胺或N,N’-二甲基乙酰胺,73-86%;聚偏氟乙烯或聚醚砜,10-15%。The components of the casting solution and their mass percentages are: dihydroxypolypropylene glycol, 1-3%, molecular weight 3000-4000; polyvinylpyrrolidone, 1-4%, molecular weight 2×10 3 ~2×10 6 ; water: 2-5%; solvent is N, N'-dimethylformamide or N, N'-dimethylacetamide, 73-86%; polyvinylidene fluoride or polyethersulfone, 10-15 %.
本发明的有益效果:Beneficial effects of the present invention:
采用孔隙率高达60-80%之间聚偏氟乙烯或聚醚砜多孔膜为骨架,电解液吸附率高,得到锂离子导电凝胶膜的电导率高。The polyvinylidene fluoride or polyethersulfone porous membrane with a porosity as high as 60-80% is used as the skeleton, the electrolyte absorption rate is high, and the lithium ion conductive gel membrane obtained has high conductivity.
又,由于在聚偏氟乙烯或聚醚砜多孔膜为骨架中共混了双羟基聚丙二醇,聚丙二醇不仅可以抑制聚偏氟乙烯或聚醚砜的结晶,而且聚电解液中的稀释剂、锂盐可以与多孔膜中的丙二醇作用,使骨架适当溶胀,吸收更多的电解液,进一步提高锂离子凝胶膜的电导率。In addition, since dihydroxypolypropylene glycol is blended in the polyvinylidene fluoride or polyethersulfone porous membrane as the skeleton, polypropylene glycol can not only inhibit the crystallization of polyvinylidene fluoride or polyethersulfone, but also the diluent in the polyelectrolyte, lithium The salt can interact with the propylene glycol in the porous membrane to properly swell the skeleton, absorb more electrolyte, and further improve the conductivity of the lithium-ion gel membrane.
又,在多孔骨架内填充含有锂盐的交联聚乙二醇凝胶,不会产生电解液泄漏,安全性提高。In addition, the cross-linked polyethylene glycol gel containing lithium salt is filled in the porous framework, so that the leakage of electrolyte solution does not occur, and the safety is improved.
又,聚丙二醇与聚偏氟乙烯或聚醚砜具有良好相容性,有利与多孔骨架形态的稳定和强度。In addition, polypropylene glycol has good compatibility with polyvinylidene fluoride or polyethersulfone, which is beneficial to the stability and strength of the porous skeleton.
又,聚丙二醇与聚偏氟乙烯或聚醚砜具有良好相容性和作用里,在相转化法制备多孔膜时使用以水为主要成分的凝固浴,能够在存留在多孔膜内。In addition, polypropylene glycol has good compatibility and interaction with polyvinylidene fluoride or polyether sulfone. When the porous membrane is prepared by the phase inversion method, a coagulation bath with water as the main component is used, and it can be retained in the porous membrane.
又,多孔骨架表面的聚丙二醇的羟基可以与电解液中交联剂反应,使多孔骨架与填充的交联聚乙二醇凝胶一体化,提高骨架与填充凝胶电解质的相容性和凝胶膜的形状稳定性。In addition, the hydroxyl group of polypropylene glycol on the surface of the porous skeleton can react with the cross-linking agent in the electrolyte, so that the porous skeleton and the filled cross-linked polyethylene glycol gel can be integrated, and the compatibility and coagulation between the skeleton and the filled gel electrolyte can be improved. The shape stability of the adhesive film.
又,在多孔骨架内填充含有锂盐的交联聚乙二醇凝胶,可以采用较高的锂盐浓度,有利于锂离子凝胶膜电导率的提高。In addition, filling the cross-linked polyethylene glycol gel containing lithium salt in the porous framework can adopt a higher concentration of lithium salt, which is beneficial to the improvement of the conductivity of the lithium ion gel membrane.
又,采用聚偏氟乙烯或聚醚砜多孔膜为骨架,锂离子凝胶膜的力学强度提高。In addition, using polyvinylidene fluoride or polyethersulfone porous membrane as the skeleton, the mechanical strength of the lithium ion gel membrane is improved.
又,采用聚偏氟乙烯或聚醚砜多孔膜为骨架,可以把多孔膜放置与电极之间,装入壳体后再用真空法注入电解液,操作方便,对环境要求低,更适合于在锂离子电池制作中使用。In addition, polyvinylidene fluoride or polyethersulfone porous membrane is used as the skeleton, the porous membrane can be placed between the electrode, and then the electrolyte is injected into the case by vacuum method. It is easy to operate and has low environmental requirements. It is more suitable for Used in the manufacture of lithium-ion batteries.
又,聚丙二醇改性聚偏氟乙烯或聚醚砜多孔膜的制备方法简单,成本低效率高,可以代替价格高的聚(偏氟乙烯-六氟丙烯)作为锂离子电池。In addition, the preparation method of polypropylene glycol modified polyvinylidene fluoride or polyethersulfone porous membrane is simple, low in cost and high in efficiency, and can replace expensive poly(vinylidene fluoride-hexafluoropropylene) as a lithium ion battery.
又,采用超支化聚合物为聚乙二醇凝胶的交联剂,电解液的粘度小/流动性好、保持液态的时间长,保证了配制好电解液后有足够的存放时间供后续使用,而且使多孔膜充分吸收电解液更加充分和最后凝胶膜电导率的提高。In addition, the hyperbranched polymer is used as the cross-linking agent of polyethylene glycol gel, the electrolyte has low viscosity/good fluidity, and keeps liquid for a long time, which ensures sufficient storage time for subsequent use after the electrolyte is prepared , and make the porous membrane fully absorb the electrolyte more fully and finally improve the conductivity of the gel membrane.
又,聚丙二醇改性的聚偏氟乙烯或聚醚砜多孔骨架中孔径大、连通性好,而且表面与孔壁上有聚丙二醇链,保证了电解液对骨架膜的充分润湿和电解液的快速吸收,提高了凝胶膜的制备效率。In addition, the polypropylene glycol-modified polyvinylidene fluoride or polyethersulfone porous skeleton has large pore size and good connectivity, and there are polypropylene glycol chains on the surface and the pore wall, which ensures that the electrolyte solution fully wets the skeleton membrane and electrolyte solution The rapid absorption improves the preparation efficiency of the gel film.
附图说明Description of drawings
图1(a)是实施例1中聚偏氟乙烯多孔骨架聚合物样品上表面的扫描电子显微镜照片;Fig. 1 (a) is the scanning electron micrograph of the upper surface of polyvinylidene fluoride porous skeleton polymer sample in embodiment 1;
图1(b)是实施例1中聚偏氟乙烯多孔骨架聚合物样品下表面的扫描电子显微镜照片;Fig. 1 (b) is the scanning electron micrograph of the lower surface of polyvinylidene fluoride porous skeleton polymer sample in embodiment 1;
图1(c)是实施例1中交联后样品导电凝胶膜样品上表面的扫描电子显微镜照片;Fig. 1 (c) is the scanning electron micrograph of sample conductive gel film sample upper surface after crosslinking in embodiment 1;
图2(a)是实施例4中聚醚砜多孔骨架聚合物样品上表面的扫描电子显微镜照片;Fig. 2 (a) is the scanning electron micrograph of the upper surface of polyethersulfone porous skeleton polymer sample in embodiment 4;
图2(b)是实施例4中醚砜多孔骨架聚合物样品下表面的扫描电子显微镜照片;Fig. 2 (b) is the scanning electron micrograph of the lower surface of the ethersulfone porous skeleton polymer sample in Example 4;
图2(c)是实施例4中交联后样品导电凝胶膜上表面的扫描电子显微镜照片;Fig. 2 (c) is the scanning electron micrograph of the upper surface of the sample conductive gel film after crosslinking in embodiment 4;
图3(a)是实施例13中聚偏氟乙烯多孔骨架聚合物样品上表面的扫描电子显微镜照片;Fig. 3 (a) is the scanning electron micrograph of the upper surface of polyvinylidene fluoride porous skeleton polymer sample in embodiment 13;
图3(b)是实施例13中聚偏氟乙烯多孔骨架聚合物样品下表面的扫描电子显微镜照片;Fig. 3 (b) is the scanning electron micrograph of the lower surface of polyvinylidene fluoride porous skeleton polymer sample in embodiment 13;
图3(c)是实施例13中交联后样品导电凝胶膜样品上表面的扫描电子显微镜照片。Fig. 3(c) is a scanning electron micrograph of the upper surface of the sample conductive gel film sample after crosslinking in Example 13.
具体实施方式Detailed ways
本发明中提出的电导率在10-3-10-2S/cm、含有多孔聚合物骨架的锂离子导电凝胶膜,原理上是通过在聚丙二醇改性的聚偏氟乙烯或聚醚砜多孔膜(也就是凝胶膜的多孔骨架)的膜孔内填充含锂离子的交联聚乙二醇凝胶、以及电解液对膜骨架的溶胀吸收实现的。所述凝胶膜的制备过程以及在锂离子电池制作中的应用方法包括四个阶段,即:多孔膜的制备、电解液的配制、多孔膜吸收电解液和凝胶化,其中,所述凝胶膜在锂离子电池制作中的应用是制备自支撑凝胶膜方法的改进和发展。The lithium-ion conductive gel membrane with a conductivity of 10 -3 -10 -2 S/cm and a porous polymer skeleton proposed in the present invention is, in principle, modified by polyvinylidene fluoride or polyethersulfone in polypropylene glycol. The membrane pores of the porous membrane (that is, the porous skeleton of the gel membrane) are filled with cross-linked polyethylene glycol gel containing lithium ions, and the membrane skeleton is swollen and absorbed by the electrolyte. The preparation process of the gel film and the application method in the production of lithium-ion batteries include four stages, namely: preparation of the porous film, preparation of the electrolyte, absorption of the electrolyte by the porous film and gelation, wherein the gel The application of gel film in the manufacture of lithium-ion batteries is the improvement and development of the method for preparing self-supporting gel film.
1.多孔膜骨架的制备1. Preparation of Porous Membrane Skeleton
采用溶液相转化法制备多孔膜,通过在铸膜液中添加聚丙二醇实现对聚偏氟乙烯、聚醚砜的改性,制备方法依次包括以下步骤:(1)配制铸膜液:将双羟基聚丙二醇、聚乙烯吡咯烷酮、水、溶剂与聚偏氟乙烯或聚醚砜混合溶解、脱气泡得到铸膜液;(2)刮制液膜:将铸膜液在不锈钢板或钢带上刮成液膜;(3)固化成膜:将带有液膜的不锈钢板浸入凝固浴固化成膜;(4)清洗干燥。The solution phase inversion method is used to prepare porous membranes, and the modification of polyvinylidene fluoride and polyethersulfone is realized by adding polypropylene glycol in the casting solution. The preparation method includes the following steps in sequence: (1) preparing the casting solution: adding dihydroxy Polypropylene glycol, polyvinylpyrrolidone, water, solvent and polyvinylidene fluoride or polyether sulfone are mixed and dissolved, and degassed to obtain a casting solution; (2) Scraping liquid film: scrape the casting solution on a stainless steel plate or steel strip to form Liquid film; (3) curing into film: immerse the stainless steel plate with liquid film in a coagulation bath to solidify into film; (4) cleaning and drying.
适合用凝胶膜作骨架的多孔膜需要具有连续的微孔通道、结构对称、膜表面开孔率高,孔径在0.2-3.0μm之间,孔隙率在60-80%之间,厚度在15-25μm之间。为了得到具有上述结构、满足凝胶膜要求多孔膜,需要通过调节铸膜液的配方、刮膜温度、固化成膜时凝固浴的组成和温度等参数。调节膜结构的原则是:采用提高铸膜液中聚乙烯吡咯烷酮的含量、降低铸膜液中聚偏氟乙烯或聚醚砜的浓度、提高凝固浴的温度、或提高凝固浴中溶剂的含量等手段制备孔径大、孔隙率高的多孔骨架膜,反之依然;通过调节刮制液膜的厚度控制多孔膜的厚度,液膜厚度大时,多孔膜的厚度大。制备相应结构多孔膜的优化条件如下:A porous membrane suitable for using gel membrane as a skeleton needs to have continuous microporous channels, symmetrical structure, high porosity on the membrane surface, pore diameter between 0.2-3.0μm, porosity between 60-80%, and thickness between 15 Between -25μm. In order to obtain a porous membrane with the above structure and meet the requirements of the gel membrane, it is necessary to adjust the formulation of the casting solution, the temperature of the scraping membrane, the composition and temperature of the coagulation bath when solidifying and forming a membrane, and other parameters. The principle of adjusting the membrane structure is to increase the content of polyvinylpyrrolidone in the casting solution, reduce the concentration of polyvinylidene fluoride or polyethersulfone in the casting solution, increase the temperature of the coagulation bath, or increase the content of solvent in the coagulation bath, etc. The method is to prepare a porous skeleton membrane with large pore size and high porosity, and vice versa; the thickness of the porous membrane is controlled by adjusting the thickness of the scraped liquid membrane. When the thickness of the liquid membrane is large, the thickness of the porous membrane is large. The optimal conditions for preparing porous membranes with corresponding structures are as follows:
铸膜液的各组成分与质量百分含量为:分子量为3400的双羟基聚聚丙二醇,2-2.5%;数均相对分子量为1×103的聚乙烯吡咯烷酮,2-3%;-N,N′-二甲基甲酰胺或N,N′-二甲基乙酰胺中的任意一种,76-82%;水:3-4%;聚偏氟乙烯或聚醚砜:11-13%。The components and mass percentages of the casting solution are: dihydroxypolypropylene glycol with a molecular weight of 3400, 2-2.5%; polyvinylpyrrolidone with a number-average relative molecular weight of 1×10 3 , 2-3%; -N , any one of N'-dimethylformamide or N,N'-dimethylacetamide, 76-82%; water: 3-4%; polyvinylidene fluoride or polyethersulfone: 11-13 %.
刮膜条件:环境温度:20-25℃。空气相对湿度为:60-80%,铸膜液温度:50-60℃。不锈钢板温度:40-50℃,液膜厚度50-100μm。Scratch film conditions: Ambient temperature: 20-25°C. The relative humidity of the air is: 60-80%, and the temperature of the casting solution: 50-60°C. Stainless steel plate temperature: 40-50℃, liquid film thickness 50-100μm.
固化条件:凝固浴成分与质量百分含量:水:30-80%,对应铸膜液中用N,N′-二甲基甲酰胺或、N,N′-二甲基乙酰胺溶剂中的任意一种:20-70%;的凝固浴温度40-50℃。Curing conditions: coagulation bath composition and mass percentage: water: 30-80%, corresponding to N, N'-dimethylformamide or N, N'-dimethylacetamide solvent in the casting solution Any one: 20-70%; the temperature of the coagulation bath is 40-50°C.
另外,为了,在清洗膜期间需要换水以充分除去多孔膜中的聚乙烯吡咯烷酮,干燥膜时需要充分除去膜中的水以避免多孔膜所含水对最后锂离子凝胶膜性能的影响。In addition, in order to change the water to fully remove the polyvinylpyrrolidone in the porous membrane during the cleaning of the membrane, it is necessary to fully remove the water in the membrane when drying the membrane to avoid the impact of the water contained in the porous membrane on the performance of the final lithium ion gel membrane.
2.自支撑锂离子导电凝胶膜的制备2. Preparation of self-supporting Li-ion conductive gel membrane
从聚丙二醇改性的聚偏氟乙烯或聚醚砜多孔膜出发,自支撑锂离子导电凝胶膜的制备包括三步操作。(1)将稀锂盐、释剂、双羟基聚乙二醇、二异氰酸酯在20℃以下混合、搅拌均匀制成电解液;(2)将多孔膜在10-20℃的电解液中浸泡10-30分钟吸收电解液;(3)将吸附盐电解液的多孔膜在60℃下处理8-10小时进行交联凝胶化。Starting from polypropylene glycol-modified polyvinylidene fluoride or polyethersulfone porous membranes, the preparation of self-supporting lithium-ion conductive gel membranes involves three steps. (1) Mix dilute lithium salt, release agent, dihydroxypolyethylene glycol, and diisocyanate below 20°C and stir evenly to make an electrolyte; (2) Soak the porous membrane in the electrolyte at 10-20°C for 10 - 30 minutes to absorb the electrolyte; (3) Treat the porous membrane absorbing the salt electrolyte at 60° C. for 8-10 hours for cross-linking and gelation.
电解液的组成对后续的电解液吸收、凝胶化反应、凝胶膜的电导率、稳定性和力学性能有重要影响。电解液的优化配方中各组分的成分和质量百分含量为:The composition of the electrolyte has an important influence on the subsequent electrolyte absorption, gelation reaction, conductivity, stability and mechanical properties of the gel film. The composition and mass percentage of each component in the optimized formula of electrolyte are:
锂盐:六氟磷酸锂或高氯酸锂中的任意一种,3-5%;Lithium salt: any one of lithium hexafluorophosphate or lithium perchlorate, 3-5%;
稀释剂:碳酸二乙酯、碳酸二甲酯或碳酸甲乙烯酯,20-30%;Diluent: diethyl carbonate, dimethyl carbonate or vinyl methyl carbonate, 20-30%;
双羟基聚乙二醇:分子量600-1000:55-70%;Dihydroxypolyethylene glycol: molecular weight 600-1000: 55-70%;
二异氰酸酯:甲苯-2,4-二异氰酸酯(TDI),二苯甲烷二异氟酸酯(MDI)或异佛尔酮二异氰酸酯(IPDI):4-6%。Diisocyanate: toluene-2,4-diisocyanate (TDI), diphenylmethane diisocyanate (MDI) or isophorone diisocyanate (IPDI): 4-6%.
OH与NCO等摩尔比Equimolar ratio of OH to NCO
另外,为保证电解液的稳定性,电解液的配置和存放需要在较低的温度下进行,防止过快出现交联凝胶化;为了保证在后续步骤中电解被多孔骨架吸充分而快速的吸收和溶胀,需要使用20-30%的稀释剂,如果稀释剂含量太高,容易出现电解液泄漏的问题;为了得到最后凝胶膜的电导率,可在保证电解液为均相的前提下增加锂盐的浓度;为了防止水汽和空气中氧气产生的不利影响,需要在无水、无氧的环境中进行凝胶膜的制备、与电极复合以及密封封装。In addition, in order to ensure the stability of the electrolyte, the configuration and storage of the electrolyte need to be carried out at a lower temperature to prevent too fast cross-linking and gelation; Absorption and swelling, need to use 20-30% diluent, if the content of diluent is too high, the problem of electrolyte leakage will easily occur; in order to obtain the conductivity of the final gel film, it can be ensured that the electrolyte is homogeneous Increase the concentration of lithium salt; in order to prevent the adverse effects of water vapor and oxygen in the air, it is necessary to prepare the gel film, compound with the electrode, and seal the package in an anhydrous and oxygen-free environment.
以下实施实例对本发明做更详细的描述,但所述实施例不构成对本发明的限制。专利中描述的性能按下列方法确定。The following examples describe the present invention in more detail, but the examples do not constitute a limitation to the present invention. The properties described in the patent are determined by the following methods.
(1)重均分子量(Mw):通过GPC根据聚苯乙烯的分子量来测量。(1) Weight average molecular weight (Mw): Measured by GPC based on the molecular weight of polystyrene.
GPC仪:WATERS高效液相色谱仪 柱子:GMHXLGPC instrument: WATERS high performance liquid chromatography column: GMHXL
溶剂:N,N-二甲基乙酰胺 温度:25℃Solvent: N,N-Dimethylacetamide Temperature: 25°C
(2)萃取效率(2) Extraction efficiency
室温下,将一定质量(m1)和大小的聚合物膜在萃取剂中萃取24h,自然干燥后称重为(m2),萃取效率按下式计算:At room temperature, a polymer film with a certain mass (m 1 ) and size was extracted in the extractant for 24 hours, and weighed as (m 2 ) after natural drying. The extraction efficiency was calculated by the following formula:
(3)孔隙率(3) Porosity
密度法测量。微孔膜干燥后裁剪出一定尺寸大小的膜,量其长、宽及厚度,称质量,由此计算膜的密度(ρm)。聚合物材料的密度(ρp)为1.77gcm-3。孔隙率按下式计算:Densitometry measurement. After the microporous membrane is dried, cut out a membrane of a certain size, measure its length, width and thickness, weigh the mass, and calculate the density (ρ m ) of the membrane. The density (ρ p ) of the polymeric material was 1.77 gcm −3 . The porosity is calculated according to the following formula:
(4)吸液率(4) Liquid absorption rate
室温下,将一定质量(m1)和大小的聚合物膜在电解质液中浸泡2h,取出后在两片滤纸间轻轻除去膜表面多余的电解质液,称重为m3,按下式计算吸液率:At room temperature, soak a polymer membrane with a certain mass (m 1 ) and size in the electrolyte solution for 2 hours, remove the excess electrolyte solution on the surface of the membrane between two pieces of filter paper after taking it out, weigh it as m 3 , and calculate it according to the following formula Absorption rate:
(5)电导率的测定(5) Determination of electrical conductivity
聚合物电解质膜的电导率采用交流阻抗法测定,将聚合物电解质膜夹在两个不锈钢电极之间,采用Solartron SI1287电化学界面仪结合SI1255B频率响应仪,HP2192a分析仪在25℃下测试,由下式计算聚
(4)(4)
其中,σ为离子电导率(S/cm),d为电解质膜的厚度(cm),Rb为电解质膜本题阻抗(Ω),A为电解质膜与电极的接触面积(cm-2)。Among them, σ is the ionic conductivity (S/cm), d is the thickness of the electrolyte membrane (cm), R b is the impedance of the electrolyte membrane (Ω), and A is the contact area between the electrolyte membrane and the electrode (cm -2 ).
(6)电导率的时间稳定性(6) Time stability of conductivity
将聚合物电解质膜放置16天,然后按(7)方法测试电导率。Place the polymer electrolyte membrane for 16 days, and then test the conductivity according to (7) method.
实施例中所用主要原料:PVDF:上海3F,FR904;聚醚砜:长春吉大高新材料有限责任公司;N,N-二甲基甲酰胺(DMF):上海经纬化工有限公司;N,N-二甲基乙酰胺(DMAc):上海经纬化工有限公司;碳酸二乙酯、碳酸二甲酯、碳酸甲乙酯:张家港国泰华荣新材料有限公司;双羟基聚丙二醇,Aldrich;丙酮:上海化学试剂总厂;六氟磷酸锂、高氯酸锂,上海化学试剂有限公司;上海化学试剂总厂;甲苯-2,4-二异氰酸酯、二苯甲烷二异氰酸酯或异佛尔酮二异氰酸酯(IPDI)上海化学试剂总厂;聚乙烯吡咯烷酮,国药集团上海化学试剂有限公司。Main raw materials used in the examples: PVDF: Shanghai 3F, FR904; polyethersulfone: Changchun Jida High-tech Materials Co., Ltd.; N, N-dimethylformamide (DMF): Shanghai Jingwei Chemical Co., Ltd.; N, N-di Methylacetamide (DMAc): Shanghai Jingwei Chemical Co., Ltd.; diethyl carbonate, dimethyl carbonate, and ethyl methyl carbonate: Zhangjiagang Guotai Huarong New Material Co., Ltd.; dihydroxypolypropylene glycol, Aldrich; acetone: Shanghai Chemical Reagents General plant; lithium hexafluorophosphate, lithium perchlorate, Shanghai Chemical Reagent Co., Ltd.; Shanghai Chemical Reagent General Factory; toluene-2,4-diisocyanate, diphenylmethane diisocyanate or isophorone diisocyanate (IPDI) Shanghai chemical reagent general Factory; polyvinylpyrrolidone, Sinopharm Shanghai Chemical Reagent Co., Ltd.
下面为含有多孔聚合物骨架的锂离子导电凝胶膜制备方法的实施例,列表中为实施例的各项实施条件,所有实施例的实施步骤均与前述实施步骤相同。The following are the examples of the preparation method of the lithium ion conductive gel membrane containing the porous polymer skeleton, and the implementation conditions of the examples are listed in the list, and the implementation steps of all the examples are the same as the aforementioned implementation steps.
实施例1:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表一所示。Example 1: The various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 1.
表1Table 1
实施例2:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表二所示。Example 2: The various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 2.
表2Table 2
实施例3:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表三所示。Example 3: The various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 3.
表3table 3
实施例4:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表四所示。Example 4: The various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 4.
表4Table 4
实施例5:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表五所示。Example 5: The various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 5.
表5table 5
实施例6:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表六所示。Example 6: The various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 6.
表6Table 6
实施例7:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表七所示。Example 7: The various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 7.
表7Table 7
实施例8:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表八所示。Example 8: The various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 8.
表8Table 8
实施例9:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表九所示。Example 9: The various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 9.
表9Table 9
实施例10:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表十所示。Example 10: Various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 10.
表10Table 10
实施例11:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表十一所示。Example 11: Various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 11.
表11Table 11
实施例12:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表十二所示。Example 12: Various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 12.
表12Table 12
实施例13:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表十三所示。Example 13: Various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 13.
表13Table 13
实施例14:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表十四所示。Example 14: Various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 14.
表14Table 14
实施例15:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表十五所示。Example 15: Various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 15.
表15Table 15
实施例16:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表十六所示。Example 16: Various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 16.
表16Table 16
实施例17:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表十七所示。Example 17: Various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 17.
表17Table 17
实施例18:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表十八所示。Example 18: Various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 18.
表18Table 18
实施例19:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表十九所示。Example 19: Various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 19.
表19Table 19
实施例20:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表二十所示。Example 20: Various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 20.
表20Table 20
实施例21:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表二十一所示。Example 21: Various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 21.
表21Table 21
实施例22:各项实施条件及所得锂离子导电凝胶膜的结构和性能如表二十二所示。Example 22: Various implementation conditions and the structure and performance of the obtained lithium ion conductive gel membrane are shown in Table 22.
表22Table 22
最后,还需要注意的是,以上列举的仅是本发明的具体实施例。显然,本发明不限于以上实施例,还可以有许多变形。本领域的普通技术人员能从本发明公开的内容直接导出或联想到的所有变形,均应认为是本发明的保护范围。Finally, it should also be noted that what is listed above are only specific embodiments of the present invention. Obviously, the present invention is not limited to the above embodiments, and many variations are possible. All deformations that can be directly derived or associated by those skilled in the art from the content disclosed in the present invention should be considered as the protection scope of the present invention.
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